This study performed second-law analysis on saturated FC - 22 vapor flowing
through and condensed in horizontal cooling tubes. An optimum Reynolds num
ber existed over the parametric range investigated for the single tube case
at which the entropy generated at a minimum rate. For the multi-tube cases
, on the other hand, no optimal Reynolds number was identified subject to c
onstant surface-area constraint. Furthermore, there was an optimal cooling
temperature that: generated a minimum of entropy for a given duty. The pres
ent phase-change system was inherently different in thermodynamic performan
ce from the single-phase convective system intensively discussed in literat
ure works.